JPS6099146A - Powdery ethylene-acrylic acid copolymer composition - Google Patents
Powdery ethylene-acrylic acid copolymer compositionInfo
- Publication number
- JPS6099146A JPS6099146A JP20804783A JP20804783A JPS6099146A JP S6099146 A JPS6099146 A JP S6099146A JP 20804783 A JP20804783 A JP 20804783A JP 20804783 A JP20804783 A JP 20804783A JP S6099146 A JPS6099146 A JP S6099146A
- Authority
- JP
- Japan
- Prior art keywords
- acrylic acid
- acid copolymer
- ethylene
- polyethylene
- composition according
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Landscapes
- Processes Of Treating Macromolecular Substances (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は粉砕性を改良したエチレン−アクリ)し酸共重
合体組成物に関する。さら昏こ詳しくはエチ粉末状の組
成物に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to ethylene-acrylic acid copolymer compositions with improved grindability. More specifically, the present invention relates to a powdered composition.
エチレン−アクリル酸共重合体(以下FAAと略す)は
従来より接着゛計、耐熱性、抗張力、耐候乙
性、耐痰音なと種々のすぐれた物理的、化学的性質のだ
4食品包装材料のラミネートフィルムやこれを粉砕して
粉体塗装用などに広く用いられている。Ethylene-acrylic acid copolymer (hereinafter abbreviated as FAA) has traditionally been used as a food packaging material with various excellent physical and chemical properties such as adhesion, heat resistance, tensile strength, weather resistance, and phlegm resistance. It is widely used for laminate films and for powder coating by crushing it.
しかしながらFAAをコーティング用(流動浸漬、静電
塗装、焼付塗装うなどの粉末にすべく粉(低温り粉砕方
こ依らねばならなかった。冷媒を用いた粉砕をすれば所
望の粉末を得ることができるが冷源(主として液体窒素
)を必要とするので経済的にネ利であり、これが簡単に
粉砕できれば経済的tこ有利な粉末を得ることができ、
従ってその用途もさらに展けるので当業界においては常
温粉砕可能なFAAの出現が望まれていた。 ″本発明
者らはこのような状況に鑑み鋭意検討を重ねた結果EA
AGこポリエチレンを少量加えれば本来有しているEA
AのJMt Hh 4.l!I注を損うことなく常温を
こおける機械粉砕がuT HQとなり従って安価な粉末
が得られることを知り本発明に到った。However, in order to turn FAA into a powder for coatings (fluidized dipping, electrostatic coating, baking coating, etc.), we had to rely on low-temperature pulverization. If we pulverized it using a refrigerant, we could obtain the desired powder. However, since it requires a cold source (mainly liquid nitrogen), it is economically disadvantageous; if it can be easily pulverized, an economically advantageous powder can be obtained.
Therefore, the industry has been hoping for the emergence of FAA that can be pulverized at room temperature, since its uses can be further expanded. ``In view of this situation, the inventors have conducted extensive studies, and as a result of the EA
If you add a small amount of AG polyethylene, the original EA
A's JMt Hh 4. l! It was discovered that mechanical pulverization, which can be heated at room temperature without impairing the I-injection properties, is uT HQ, and therefore an inexpensive powder can be obtained, leading to the present invention.
即ち本発明の目的は常温粉砕容易なFAA樹脂組成物を
提供することにあり、その要旨はエチレ°ンーアクリル
酸共重合体昏こポリエチレンを等量以下の量混練、混杏
、粉砕してなる粉末状のエチレン−アクリル酸共重合体
組成物である。That is, the object of the present invention is to provide an FAA resin composition that is easily pulverized at room temperature. This is an ethylene-acrylic acid copolymer composition.
本発明で用いるEAAはエチレンのフリーラジカルとア
クリル酸との高圧反応によって共重合させ装造される。EAA used in the present invention is prepared by copolymerizing ethylene free radicals and acrylic acid through high-pressure reaction.
将にEAA中のアクリル酸含量が1〜20@11%のも
のが本発明の目的に適している。Generally, EAA with an acrylic acid content of 1 to 20@11% is suitable for the purpose of the present invention.
本発明において使用するポリエチレンは高圧法低密度ポ
リエチレン直輪状低密度ポリエチレンの1’++Jれで
もよくそのメルトインデックスが2〜70程度のものを
その目的に応じ°C適宜選定して使用する。The polyethylene used in the present invention may be high-pressure low-density polyethylene or rectangular low-density polyethylene having a melt index of about 2 to 70 at a suitable temperature depending on the purpose.
FAAとポリエチレンの配合比は90〜55:10−4
5の範囲のものが本発明の10月こ適している。EAA
が少ないとその特性が現れず、多過ぎると常温粉砕しに
くい。The blending ratio of FAA and polyethylene is 90-55:10-4
A range of 5 is suitable for the present invention. EAA
If there is too little, the characteristics will not be exhibited, and if there is too much, it will be difficult to grind at room temperature.
EAAとポリエチレンとの混練方法としては熱ロール、
ニーグー、バンバリーミキサ−あるいは押出機を用いる
メルトミックス法が用いられ、待※こ押出機を用いて混
練し水冷ペレット化するのが便利であり好ましい。The kneading method for EAA and polyethylene is hot roll,
A melt mix method using a Negoo mixer, a Banbury mixer, or an extruder is used, and it is convenient and preferable to knead and water-cool pellets using a stand-off extruder.
この際粉体塗装用樹脂に通常用いられる安定剤。In this case, a stabilizer is commonly used in powder coating resins.
滑剤、紫外線吸収剤などの添加剤の外、顔料、染料など
の着色剤を同時に混合することができその処方は目的蚤
こ応じて決定する。In addition to additives such as lubricants and ultraviolet absorbers, coloring agents such as pigments and dyes can be mixed at the same time, and the formulation is determined depending on the intended flea.
混練後目的をこ応じ”で所定の大きさに粉砕するが本発
明においては常温において機械粉砕できるのが特徴であ
り、粉砕繍としては従来市販の衝撃型もしくは摩砕型の
ものを適宜使用することができる。After kneading, the material is pulverized to a predetermined size according to the purpose.The feature of the present invention is that it can be mechanically pulverized at room temperature, and conventional commercially available impact type or grinding type can be used as appropriate. be able to.
粉末の大きさは通常粒径1000〜50μ(20〜25
0メツシユ)程度のものを用いるが、流動浸漬用として
は中位粒度50〜80 メツシュ程度のものが好ましい
。The size of the powder is usually 1000~50μ (20~25μ).
For fluidized dipping, a medium particle size of about 50 to 80 mesh is preferred.
粉末コーティング方法とし又は流動浸漬法1静電塗装法
、まぶし法など特に限定されることなく製品の種類、大
きさ、経済1士などを考慮して決定すべきであるが−プ
役に流動浸漬法を用いる場合が多い。Powder coating method or fluid dipping method 1 Electrostatic coating method, sprinkling method etc. There are no particular limitations and the decision should be made in consideration of the product type, size, economics, etc. The law is often used.
以下実施例tこより本発明を具体的に説明するが本発明
が実施例により限定されるものでないことは云うまでも
ない。The present invention will be explained in detail below using Example t, but it goes without saying that the present invention is not limited to the Examples.
実施例1
gAA(アクリル酸含は6.6%; M I 9・0;
商、arw−x −h C1yX −1an :8 ン
+l+ イv、s= ) 10n 〜 in重喰部と直
鎖低密度ポリエチレン(商品名NZ−25100;三井
石油化学装、MIIO)0〜50重量部を径iooグL
/D : 25の押出機を140°Cに保って練り込み
押出して水冷ペレット化したものを常温で機械粉砕した
。Example 1 gAA (acrylic acid content: 6.6%; M I 9.0;
quotient, arw-x -h C1yX -1an:8 + l + iv, s = ) 10n ~ in Heavy weight part and linear low density polyethylene (product name NZ-25100; Mitsui Petrochemical Systems, MIIO) 0 ~ 50 weight The diameter of the part is L
/D: The extruder No. 25 was kept at 140° C. to knead and extrude the resulting water-cooled pellets, which were then mechanically pulverized at room temperature.
その粉末物性を従来の冷凍扮砕品と対比して第1表に示
す。またこの粉砕の結果を第2表に示す。The physical properties of the powder are shown in Table 1 in comparison with conventional frozen crushed products. The results of this pulverization are also shown in Table 2.
なお本発明4二よる組成物の物性をFAAと比較して第
8表に示す。The physical properties of the composition according to the present invention 42 are shown in Table 8 in comparison with those of FAA.
第1表
第2表
第 3 表
実施#!A2
E A A (7り’) )’融合な8%、MI=9.
Q:j論者 F A A −4590t)y Chem
lea1社製)xoo〜50重量部と高圧法低密度ポリ
エチレン、(商品名久ミカセ:/G −701M I
= 7住友化学製)o 〜50爪量部を押出して水冷ペ
レット化したものを常温で機械粉砕した。その粉砕結果
を第4表、455表)こ示す。Table 1 Table 2 Table 3 Implementation #! A2 E A A (7ri') )' fusion 8%, MI=9.
Q: J-argument F A A -4590t)y Chem
(manufactured by Lea1) xoo ~ 50 parts by weight and high pressure low density polyethylene (trade name: Kumikase: /G-701M I
= 7 (manufactured by Sumitomo Chemical) o ~50 parts were extruded and made into water-cooled pellets, which were mechanically pulverized at room temperature. The pulverization results are shown in Tables 4 and 455).
iJ4表
実施例3
FAA(アクリル咽含敏12%、MI17.商品名:
ユカo ンX −192三菱油化*)100〜50重量
部と低密度ポリエチレン(商品名: 0220200M
I20.三井石油化製)θ〜50i量部を押出し水冷ペ
レット化したものを常温機械粉砕した。その粉砕結果を
第6表、第7表に示す。iJ4 Table Example 3 FAA (acrylic throat absorbent 12%, MI17.Product name:
100 to 50 parts by weight of Yukan-X-192 Mitsubishi Yuka*) and low-density polyethylene (product name: 0220200M)
I20. (manufactured by Mitsui Petrochemical) θ~50i parts were extruded and made into water-cooled pellets, which were mechanically pulverized at room temperature. The pulverization results are shown in Tables 6 and 7.
第6表
第7表
このように不発明の組成物は粉砕性が良好であり、粉末
物性ならびに流動浸漬をこよる流動性も良好でコーティ
ングしたものは強(1,接着性を維持し被膜物性もEA
A単独品をこ比して遜色なく粉末加工用として光分使用
でさるものであった。Table 6 Table 7 As shown above, the uninvented composition has good pulverizability, good powder physical properties and good fluidity due to fluid dipping, and the coated one has strong properties (1, maintaining adhesion and coating physical properties). Also EA
It was as good as the product A alone and could be used for powder processing using light.
出願人製鉄化学工業株式会社 代表者 佐々木 浩Applicant Steel Chemical Industry Co., Ltd. Representative Hiroshi Sasaki
Claims (8)
を等量以下の量を混練、混合、粉砕してなる粉末状のエ
チレン−アクリル酸共重合体組成物。(1) A powdery ethylene-acrylic acid copolymer composition obtained by kneading, mixing, and pulverizing ethylene-acrylic acid copolymer and polyethylene in equal or less amounts.
量が1〜20重量%である特許請求の範囲(1)記載の
組成物。(2) The composition according to claim (1), wherein the acrylic acid content of the ethylene-acrylic acid copolymer is 1 to 20% by weight.
の配合比が90〜55:10−45である特許請求の範
囲(1)記載の組成物。(3) The composition according to claim (1), wherein the blending ratio of the ethylene-acrylic acid copolymer and polyethylene is 90-55:10-45.
L−LDPK )である特許請求の範囲(1)記載の組
成物。(4) Low-density polyethylene with linear polyethylene (
The composition according to claim (1), which is L-LDPK).
る特許請求の範囲(1)記載の組成物。(5) The composition according to claim (1), wherein the polyethylene is high-pressure low-density polyethylene.
に粉砕した特許請求の範囲(1)記載の組成物。(6) The composition according to claim (1), which is kneaded using an extruder and then mechanically pulverized without using a refrigerant.
特許請求の範囲(6)記載の組成物。(7) The composition according to claim (6), wherein the mechanical crushing is by impact or grinding.
の範囲(11,(61または(7)記載の組成物。(8) The composition according to claim 11, (61 or (7)), wherein the particle size of the powder is 50-1000μ.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP20804783A JPS6099146A (en) | 1983-11-04 | 1983-11-04 | Powdery ethylene-acrylic acid copolymer composition |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP20804783A JPS6099146A (en) | 1983-11-04 | 1983-11-04 | Powdery ethylene-acrylic acid copolymer composition |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6099146A true JPS6099146A (en) | 1985-06-03 |
JPH0116429B2 JPH0116429B2 (en) | 1989-03-24 |
Family
ID=16549760
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP20804783A Granted JPS6099146A (en) | 1983-11-04 | 1983-11-04 | Powdery ethylene-acrylic acid copolymer composition |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6099146A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1999025776A1 (en) * | 1997-11-14 | 1999-05-27 | E.I. Du Pont De Nemours And Company | Particles and process for corrosion- and creep-resistant coatings |
JP2008063539A (en) * | 2006-09-11 | 2008-03-21 | Du Pont Mitsui Polychem Co Ltd | Thermoplastic resin composition and use thereof |
-
1983
- 1983-11-04 JP JP20804783A patent/JPS6099146A/en active Granted
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1999025776A1 (en) * | 1997-11-14 | 1999-05-27 | E.I. Du Pont De Nemours And Company | Particles and process for corrosion- and creep-resistant coatings |
AU752623B2 (en) * | 1997-11-14 | 2002-09-26 | E.I. Du Pont De Nemours And Company | Particles and process for corrosion- and creep-resistant coatings |
JP2008063539A (en) * | 2006-09-11 | 2008-03-21 | Du Pont Mitsui Polychem Co Ltd | Thermoplastic resin composition and use thereof |
Also Published As
Publication number | Publication date |
---|---|
JPH0116429B2 (en) | 1989-03-24 |
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